Preparation aroma system for dehydrated food product compositions

ABSTRACT

A particulate food preparation aroma composition and dehydrated food or beverage composition including the particulate preparation aroma composition. The particulate composition includes a food aromatizing composition which comprises a volatile characterizing food aroma constituent other than a natural essential oil and a volatile organic carrier which is in the liquid state at 25° C. and atmospheric pressure and has a vapor pressure of at least 0.01 mm Hg at 25° C., a boiling point in the range of 25 to 250° C., a density of less than 1.0 g/cc at 25° C., and water solubility of not more than about 10% at 25° C.

FIELD OF THE INVENTION

The invention relates to compositions for providing aroma at the time of preparation of a food from a dehydrated food composition, to dehydrated food compositions containing such aromatizing compositions, and to methods of preparing foods from said dehydrated food compositions.

BACKGROUND OF THE INVENTION

The production of dehydrated food compositions often involves processing conditions such as elevated temperature, which causes loss of desirable food aroma. One known technique of overcoming such loss is to add additional aroma and flavor to dehydrated foodstuffs and beverages. There is an abundance of art on the preparation of natural and artificial aromas and flavors for addition to dehydrated foodstuffs or beverages. Such aromas and flavors are usually complex, comprising many organoleptically active compounds, which combine in effect to create the characterizing aroma of the product. Since aromas and flavors are extremely powerful and typically unstable in their undiluted state they are combined with a carrier to render them stable and easier to handle. The carriers are neutral or complementary in organoleptic impact and do not contribute to the characterizing aroma of the product.

Carriers can be water-soluble solids or liquid. In cases where a liquid carrier is used, it is often encapsulated in a solid, water-soluble matrix to further preserve the characterizing aromas from loss or damage. The carrier, often referred to as a solvent in liquid systems, functions as an aroma base and is used to adjust the level of otherwise powerful aroma and taste substances to levels similar to those that exist in nature. Desirable characteristics of carriers for liquid systems include blandness and miscibility with other liquid carriers and with liquid aromas. Traditional carriers include ethanol, propylene glycol, glycerol, vegetable oil, benzyl alcohol, triacetin, tripropionin, triethyl citrate, and tributyrin.

The aroma constituent of an aromatizing composition characterizes its aroma, i.e., the innate quality that gives the aroma its special attributes among and over other aromas. The aroma constituent may, and often does, include a plurality of aroma ingredients which together result in the characterizing aroma.

When a preparation aroma is desired upon rehydration of such flavors and aromas in a dehydrated food or beverage such composition are limited in effectiveness because of poor aroma release. When a solid carrier is used, the release or aroma is poor because the diffusion of rehydrating liquid into the particle during rehydration inhibits the counter-diffusion of aroma out. In this way the vast majority of the characterizing aroma constituents end up in therehydrating liquid. An aroma burst can be obtained by increasing the loading of characterizing aroma constituents into the carrier but this typically leads to an overwhelmingly strong or unbalanced flavor in the product when consumed.

Likewise poor aroma release is obtained when traditional liquid carriers are used, whether or not they are encapsulated. Those which are water-soluble, suffer the same problems as with soluble solid carriers. The flux of water into the carrier inhibits the diffusion of the aromas out. Furthermore many carriers have a density greater than 1.0 g/cc so they sink in the product during hydration and aromas are released into the rehydrating liquid rather than being released at the surface to effect preparation aroma. Finally those conventional carriers which do float and are insoluble in water are of an oily or fattynature. Though these can be arranged to release aroma at the surface they leave an unsightly and often organoleptically and visually undesirable “slick” at the surface of the product.

Natural essential oils from botanical sources are typically intensely flavored and naturally aromatic due their inherent volatility. This makes them an ideal choice as aromatizing constituents for use in the manufacture of food products. Unfortunately, volatile essential oils do not exist in all food sources used to manufacture food products. In addition, essential oils that do occur naturally in some foods are often not sufficiently abundant or readily extracted to permit their economical use in processed foods, and some are not approved for food use. Furthermore, many processed foods, due to their intended use, are not able to be manufactured with natural food ingredients that may contain essential oils.

For example, instant beverage powders typically must quickly and completely dissolve in water without producing insoluble floating or suspended matter or sediment in order to be acceptable to the consumer, and foods or ingredients derived from foods that do contain naturally occurring volatile oils typically are not completely water soluble. In response to these limitations, natural or synthetic flavoring agents are typically used to impart the desired character and identity to such food products. In many cases, especially when economically favored, the flavoring agent may contain a natural essential oil, such as in the widespread use of encapsulated orange oil powders used to flavor imitation or orange-flavored instant beverages. Orange oil is readily and economically pressed from discarded orange peels, an abundant byproduct of the orange juice industry.

One well known example of food processing that results in loss of aroma is the manufacture of “instant” (or soluble) coffee powder. Unless additional steps are taken in its manufacture, there is very little aroma associated with hot coffee beverages prepared from instant coffee powder relative to the aroma of hot coffee beverages prepared by brewing roast and ground coffee. Many attempts have been made to enhance the aroma of instant coffee products, including the use of particular types of coffee beans, the use of particular coffee roasting conditions, and the addition of coffee aroma.

A particular problem which has been noted in connection with instant coffee is the relative lack of coffee aroma that is generated at the time that a hot instant coffee beverage is prepared compared to the coffee aroma that is generated when brewing coffee. This problem of poor preparation aroma (i.e., poor aroma burst or “above-cup aroma” at the time of preparation of an instant coffee beverage) is noted in U.S. Pat. No. 5,399,368 assigned to Nestec S.A. and in U.S. Pat. No. 5,750,178 also assigned to Nestec S.A. Each of these patents describes several prior art attempts to provide an initial burst of above-cup coffee aroma, such as by coating soluble coffee powder with an aqueous emulsion of an aromatic coffee substance, or by employing particulate aromatized coffee glass. It is reported in each of these U.S. patents that these and other previously known procedures had not been successful in achieving good preparation aroma. The '368 patent proposes a method of coextruding capsule particles in which a liquid core material containing aromatized coffee oil is encapsulated within a shell of hardened coffee glass. The shell encapsulates a core of aromatized coffee oil saturated with an inert gas under pressure. The '178 patent also describes known techniques for aromatizing instant coffee and notes that techniques which may provide good package aroma (i.e., aroma in a coffee container) do not provide good preparation aroma. The '178 patent reports that the method of the '368 patent provides excellent entrapment of the aroma but that complex machinery and careful control are required. The '178 patent proposes a modified method of preparing the aromatized coffee capsule particles which method is said to have the advantage of simplicity.

The amount of preparation aroma which can be achieved by incorporating aromatized coffee particles, such as those described in the '368 and '178 patents, in an instant coffee product, depends in part on the amount of such particles employed. Good preparation aroma can be achieved by employing a sufficient amount of the aromatized capsules. However, the more capsules that are employed, the more capsule material, particularly coffee oil, that is introduced. The added coffee oil accumulates as an oil film on the surface of the coffee beverage. Such oil films are readily apparent and are widely known to impair consumer acceptance of instant coffee.

A need arises to provide good food preparation aroma without requiring the use of natural essential oils or the use of amounts of other ingredients, such as vegetable oils, that would adversely affect the properties of foods prepared from the food product compositions. A particular need arises to provide such good preparation aroma for dehydrated hot beverage and soup compositions.

SUMMARY OF THE INVENTION

In one aspect, the invention provides a particulate food preparation aroma composition comprising particles having a solid, water soluble matrix, said matrix having physically entrapped therein a food aromatizing composition, said food aromatizing composition comprising a volatile characterizing food aroma constituent other than a natural essential oil, and a volatile organic carrier, said volatile organic carrier being in the liquid state at 25° C. and atmospheric pressure, having a vapor pressure of at least 0.01 mm Hg at 25° C., a boiling point in the range of 25 to 250° C., a density less than 1.0 g/cc at 25° C., and water solubility of not more than about 10% at 25° C.

In a further aspect, the invention provides a dehydrated food or beverage product composition comprising a food ingredient and a particulate food preparation aroma ingredient for providing a burst of aroma at the time of preparing a food or beverage from said dehydrated food or beverage product composition, said food preparation aroma ingredient comprising particles having a solid, water soluble matrix, said matrix having physically entrapped therein a food aromatizing composition, said food aromatizing composition comprising a volatile characterizing food aroma constituent other than a natural essential oil, and a volatile organic carrier, said volatile organic carrier being in the liquid state at 25° C. and atmospheric pressure, having a vapor pressure of at least 0.01 mm Hg at 25° C., a boiling point in the range of 25 to 250° C., a density less than 1.0 g/cc at 25° C., and water solubility of not more than about 10% at 25° C.

In a still further aspect, the invention provides a method of preparing a food or beverage from a dehydrated food or beverage product composition, which comprises providing a dehydrated food product composition comprising a food ingredient and a food preparation aroma ingredient for providing a burst of aroma at the time of preparing a food or beverage from said dehydrated food or beverage product composition, said food preparation aroma ingredient comprising particles having a solid, water soluble matrix, said matrix having physically entrapped therein a food aromatizing composition, said food aromatizing composition comprising a volatile characterizing food aroma constituent other than a natural essential oil and a volatile organic carrier, said volatile organic carrier being in the liquid state at 25° C. and atmospheric pressure, and having a vapor pressure of at least 0.01 mm Hg at 25° C., a boiling point in the range of 25 to 250° C., a density less than 1.0 g/cc at 25° C., and water solubility of not more than 10% at 25° C. and hydrating said food product composition at a food preparation temperature.

DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS

The term “food” when used in conjunction with “beverage”, such as in the expression “food or beverage” is used to distinguish a food product such as soup from a beverage product such as a coffee beverage. The term “food” when not used in conjunction with the term “beverage”, such as in the expression “food product composition” includes beverages.

The expressions “natural food aroma” and “synthetic food aroma” as used herein have the same meanings, respectively, as “natural flavor” and “artificial flavor” as defined by the U.S. Food and Drug Administration (Code of Federal Regulations, Title 21, paragraph 101.22 and (a)(3) and (a)(1).

The release of aroma during food preparation affects the desirability and enjoyment of most foodstuffs. The intensity of preparation aroma can significantly impact the consumer's perception of product freshness and quality. Heightened preparation aroma intensity can usually be achieved by simply increasing the amount of volatile aroma formulated into a food product. However, the normal amount must typically be increased many fold to produce a noticeable effect on preparation aroma. Unfortunately, this approach often leads to a product having overwhelmingly strong taste or aroma during consumption. The present invention provides a more intense preparation aroma while seeking to avoid deleterious effects on quality. In one embodiment, a particulate aroma composition may be used to provide the consumer with two distinct and desirable aroma experiences. Intense aroma, derived from the high release efficiency of the novel aroma system described herein, may be perceived during food preparation, and normal-strength aroma and flavor, more typical of widely used low release efficiency conventional aroma systems, may be perceived during subsequent consumption.

The invention combines a volatile food aroma other than a natural essential oil, with a volatile, organic carrier resulting in a volatile aromatizing composition for use in dehydrated food product compositions. The invention enables the production of compositions which can be viewed as synthetic versions of essential oils in a form which can be used to deliver preparation aroma in processed food applications where use of natural essential oils is discouraged or prohibited due to one or more of the availability, cost, or product compatibility issues discussed above. The use of a novel volatile carrier, having the present combination of physical properties is key to the present invention and clearly distinguishes it from flavoring agents, either natural or artificial, which utilize traditional carriers. Traditional carriers are either too water soluble, have density greater than 1 g/cc, or are not sufficiently volatile to provide the preparation aroma impact desired while avoiding oily surface residues and potentially adverse effects on flavor. The volatile aromatizing composition is biphasic with water and has a temporary existence at the temperature of food preparation. This creates a beneficial non-equilibrium environment in which both the aroma and carrier evaporate from floating oil-like droplets that will disappear from the surface of a beverage or other food product, particularly those prepared by combining an aqueous liquid such as water or milk with a dry-mix food product composition. The volatile aromatizing composition is physically entrapped, preferably by encapsulating, in solid, water soluble particles to reduce evaporation and oxidation during storage. The particulate aroma composition is readily incorporated into and packaged with dehydrated food product compositions, particularly dry-mix food compositions such as hot or cold dry-mix beverage or soup compositions.

The use of the present volatile organic carriers may provide several advantages. Since the volatile organic carrier is at most sparingly water-soluble and has a density less than the density of water, it will float to the surface of food products such as aqueous beverages, where it can release aroma directly into the air above the food product at the time that it is prepared. This effect is desirable since it will serve to minimize loss of aroma by dissolution, and maximize the intensity of aroma perceived by the consumer. Also, since volatile carriers rapidly evaporate along with the aroma, they do not leave behind an undesirable oil slick on the surface of the food as occurs in applications that utilize non-volatile carriers such as vegetable oil.

Volatile carriers typically also have much lower freezing point and viscosity than edible oils, typically vegetable oils, which allow them to be aromatized by direct contact with cold or frozen flavors. An example is contact of the carrier with a coffee aroma frost. Aromatization at low temperature can be advantageous to reduce loss of very volatile aromas by evaporation and to reduce loss of labile aromas by thermal or oxidative degradation. Other solvents that have lower freezing points than edible oils, such as triacetin, benzyl alcohol, propylene glycol, or ethanol, typically have high water solubility and/or density greater than water, properties that will tend to reduce initial aroma burst. Another advantage is that the volatile organic carriers may be used as a solvent to extract aroma directly from natural sources. They can then be easily distilled and condensed to facilitate concentration or fractionation of aromas.

The invention has particular utility in providing good above-cup aroma in the preparation of a hot aqueous beverage, such as coffee, cappuccino, tea, or cocoa, from a powdered instant beverage composition without adversely affecting other properties of the beverage. Such beverages are generally prepared by combining the powder with hot water or milk at elevated temperature, typically at about 75-100° C., usually at about 85-100° C.

It is an essential feature of the invention that the food aromatizing composition includes a volatile organic carrier for the food aroma that is volatile at the temperature of food preparation. More than one such carrier may be employed. The carrier has a vapor pressure of at least 0.01 mm Hg at 25° C. and a boiling point in the range of from 25° C. to 250° C., and is in the liquid state at 25° C. and atmospheric pressure. Accordingly, the carrier can be vaporized at the food product preparation temperature of the food product composition which utilizes the aromatized carrier. The carrier preferably has a vapor pressure of at least 0.5 mm Hg at 25° C., more preferably at least 2 mm Hg at 25° C., and most preferably at least 5 mm Hg at 25° C. For hot beverage and soup compositions, preferred carriers have a boiling point in the range of 25-200° C., and more preferred carriers have a boiling point in the range of 25-100° C. For cold food product compositions such as beverages and desserts, preferred carriers have a boiling point in the range of 25-50° C.

Density of the carrier is sufficiently low to enable droplets of the aromatized carrier to float in order to enhance the aroma burst. Carrier density values herein are at 25° C. unless otherwise stated. Carrier density is suitably less than 1.0 g/cc, preferably from 0.7 to 0.99 g/cc, and more preferably from 0.8 to 0.95 g/cc.

Water solubility of the carrier is preferably sufficiently low to minimize loss of aroma burst due to dissolution of the carrier into an aqueous liquid utilized to prepare the food product. However, in many instances a good aroma burst can be obtained when the carrier is partially water soluble. For example, a good aroma burst can often be achieved with such carriers when the aromatized particles float, particularly if the absolute density of the floating particles is not more than about 0.95 g/cc. In general, water solubility of the carrier is not greater than about 10% at 25° C., and is preferably not greater than about 5% at 25° C. Most preferably, the carrier is water insoluble.

Suitable volatile carriers include the following:

Vapor Boiling Freezing Insoluble Pressure* Density Point Point Water Novel Volatile Carriers (mm Hg) (g/cc) (° C.) (° C.) Solubility Chemical Classification 2-methylfuran ˜260 0.91 63 −89 insoluble furan 2,5-dimethylfuran ˜50 0.90 92 −62 insoluble furan 2-ethylfuran 50 0.91 92 <−70 insoluble furan isobutyl propionate ˜6.2 0.87 137 −71 insoluble ester methyl hexanoate ˜4.0 0.89 151 −71 insoluble ester ethyl hexanoate ˜1.5 0.87 168 −67 insoluble ester heptyl acetate ˜0.4 0.86 192 −50 insoluble ester methyl octanoate ˜2.7 0.88 195 −40 insoluble ester heptyl acetate ˜0.4 0.88 193 −50 insoluble ester ethyl octanoate ˜0.3 0.88 209 −47 insoluble ester octyl acetate ˜0.6 0.87 199 −80 insoluble ester methyl decanoate ˜0.04 0.87 224 −18 insoluble ester methyl undecanoate ˜0.03 0.89 248 insoluble ester heptyl butanoate ˜0.05 0.86 226 −58 insoluble ester ethyl decanoate ˜0.04 0.86 245 −20 insoluble ester heptanal ˜2.5 0.82 153 −43 insoluble aldehyde octanal ˜2.4 0.83 173 −12 insoluble aldehyde nonanal ˜0.6 0.83 191 insoluble aldehyde decanal ˜0.2 0.83 210 −5 insoluble aldehyde 1-heptanol ˜0.2 0.82 175 −35 insoluble aliphatic alcohol 1-octanol ˜0.05 0.83 195 −16 insoluble aliphatic alcohol 2-octanol ˜0.5 0.82 179 −39 insoluble aliphatic alcohol 1-nonanol ˜0.2 0.83 215 −6 insoluble aliphatic alcohol 2-pentanone 37 0.81 102 −77 insoluble ketone 3-heptanone ˜3.7 0.82 149 −39 insoluble ketone 3-octanone ˜2.5 0.82 168 insoluble ketone 2-nonanone ˜0.4 0.83 196 −7 insoluble ketone p-cymene 1.4 0.85 178 −69 insoluble monoterpene hydrocarbon myrcene ˜2.5 0.79 167 insoluble monoterpene hydrocarbon d-limonene 2.1 0.84 175 −74 insoluble monoterpene hydrocarbon l-limonene ˜1.8 0.84 176 insoluble monoterpene hydrocarbon dipentene ˜2.0 0.84 176 −95 insoluble monoterpene hydrocarbon terpinolene ˜0.7 0.86 185 insoluble monoterpene hydrocarbon O-pinene 4.8 0.86 155 −64 insoluble monoterpene hydrocarbon π-pinene 4.6 0.87 167 −61 insoluble monoterpene hydrocarbon O-phellandrene ˜2.0 0.85 172 insoluble monoterpene hydrocarbon π-phellandrene ˜1.8 0.85 172 insoluble monoterpene hydrocarbon isoprene ˜580 0.68 34 −147 insoluble hydrocarbon n-pentane 512 0.62 36 −130 insoluble hydrocarbon n-hexane ˜225 0.66 69 −95 insoluble hydrocarbon n-heptane 46 0.68 98 −91 insoluble hydrocarbon n-octane 14 0.70 126 −57 insoluble hydrocarbon n-nonane ˜3.5 0.72 151 −51 insoluble hydrocarbon n-decane ˜1.8 0.73 174 −30 insoluble hydrcarbon n-undecane ˜0.4 0.74 196 −26 insoluble hydrocarbon dibutyl ether 12.5 0.76 142 −98 insoluble ether ethyl propyl ether ˜210 0.74 64 −79 insoluble ether dipentyl ether ˜1.1 0.78 190 −69 insoluble ether Vapor Boiling Freezing Slightly Soluble Novel Pressure* Density Point Point Water Volatile Carriers (mm Hg) (g/cc) (° C.) (° C.) Solubility Chemical Classification ethyl formate ˜240 0.92 54 −79 slight (8%) ester ethyl acetate 94 0.90 77 −84 slight (8%) ester propyl formate ˜82 0.90 82 −93 slight (2%) ester methyl propionate ˜86 0.91 80 −87 slight (5%) ester ethyl propionate ˜37 0.89 99 −74 slight (1%) ester propyl acetate 34 0.89 102 −93 slight (1%) ester isopropyl acetate 61 0.87 89 −73 slight (4%) ester isobutyl formate ˜42 0.88 99 −96 slight (1%) ester isobutyl acetate ˜20 0.87 117 −99 slight (1%) ester ethyl butanoate ˜17 0.88 120 −93 slight (1%) ester methyl pentanoate ˜14 0.88 128 slight ester n-butyl acetate 12.4 0.88 126 −78 slight (1%) ester propyl butanoate ˜5.7 0.87 143 −97 slight ester isobutyl butanoate ˜4.0 0.86 158 slight ester isobutyl isobutanoate ˜4.5 0.83 157 −81 slight ester methyl heptanoate ˜1.4 0.87 173 −56 slight ester 2-methylpropanal ˜250 0.79 64 −66 slight (8%) aldehyde 3-methylbutanal ˜40 0.78 92 −51 slight aldehyde hexanal ˜15 0.82 128 −56 slight aldehyde pyrrole 8.2 0.97 130 −23 slight pyrrole 1-butanol 6.4 0.81 118 −90 slight (7%) aliphatic alcohol 1-pentanol 1.9 0.81 138 −79 slight (3%) aliphatic alcohol 1-hexanol ˜1.0 0.82 157 −52 slight (8%) aliphatic alcohol 2-heptanone ˜2.5 0.82 151 −35 slight ketone 2-octanone ˜1.0 0.82 172 −16 slight ketone methyl propyl ether ˜455 0.73 39 slight (4%) ether dipropyl ether ˜70 0.74 91 −122 slight (1%) ether *Includes values reported in the literature and estimates based on available data. Vapor pressure, density and water solubility (weight %) reported at 25° C.. Not all compounds listed are approved for food use.

The volatile carriers suitable for this invention are preferably bland, but may have an inherent aroma. The amount of aroma generated by the carrier is generally small relative to the aroma generated by the food aroma constituent of the volatile aroma system of the invention. In some cases, the inherent aroma of the carrier will be essentially undetectable. In any event, inherent aroma of a volatile carrier may be reduced by conventional deodorizing techniques such as by adsorption, extraction, or distillation. However, it is possible to select a volatile carrier which has an inherent aroma which is appropriate for a food or beverage prepared from the food or beverage product composition in which the carrier is utilized. For example, furan and a variety of alkyl substituted furans such as 2-methylfuran, 2-ethylfuran, and 2,5dimethylfuran occur naturally in coffee at extremely low levels in combination with a wide variety of other compounds, and, when obtained from coffee, have coffee compatible aroma. These furans do not occur naturally in coffee in sufficient quantity to be used economically as volatile carriers, but they can be readily obtained from other sources. A carrier with a fruity aroma, such as non-deodorized d-limomene which has a mild citrus aroma, is a suitable carrier for aromas for dehydrated fruit-flavored food or beverage products.

The amount of carrier in the aromatizing composition may vary widely. In general, the carrier is present in an amount of at least 25% by weight, based on the total weight of the carrier and the aroma constituent. Ordinarily the amount of carrier will exceed 35% by weight on the same basis and will often exceed that of the aroma constituent such that it will be present in an amount of more than 50% by weight based on the total weight of the carrier and the aroma constituent. Correspondingly, the amount of the aroma constituent may also vary widely, suitably up to 65 or 75% by weight based on the total weight of the carrier and aroma constituent and will often be present in an amount of less than 50% by weight on the same basis.

The volatile food aroma constituent of the invention may include any synthetic or natural food aroma other than a natural essential oil. Natural volatile food aroma compounds other than natural essential oils may be obtained from vegetables, fruits, seafood, milk, meat, spices, beans, nuts, seeds, cereal grains, flowers, roots, tubers, etc.

The food aroma constituent can be incorporated into the food aromatizing composition in any convenient way such as by simple mixing with the carrier. The aroma constituent is usually in a liquid or solid state but may be gaseous. For use in instant coffee products, the aroma constituent preferably is or includes natural coffee aroma gas, liquid or frost obtained from coffee processing. It is a distinct advantage of the invention that because the volatile carriers generally have a low freezing point, the carrier can be aromatized without heating to an elevated temperature. This is advantageous because food aroma is generally adversely affected by higher temperatures. The ability to aromatize without raising temperature above ambient is particularly advantageous in connection with coffee products because it permits aromatization of a liquid carrier by simply introducing coffee aroma frost into the carrier at room temperature or at a lower temperature down to the melting point of the aroma frost.

The food aroma is preferably soluble in the carrier. Where the aroma is not completely soluble, one or more suspending agents, emulsifiers, or co-solvents may be included to form a homogenous mixture, prior to physically entrapping the aromatizing composition in solid particles. As used herein, the term “mixture” as applied to the aromatizing composition, is intended to include compositions in which the aroma constituent is dissolved, suspended, or emulsified.

Preferred food aromas include food aromas for liquid food products, particularly instant soups and beverages, more particularly hot instant soups and beverages. However, the particulate aromatizing agents of the invention can be used to aromatize other food products, such as instant puddings and other desserts, and various frozen food products such as frozen pizza that would normally be reconstituted with hot water or milk or heated by the consumer prior to consumption. Accordingly, the food aroma can be, for example, a cheese aroma suitable for cheese-containing food products. Suitable food aromas include the following:

for hot soluble coffee-based beverages: coffee, hazelnut, amaretto, chocolate, cream and vanilla;

for hot soluble tea-based beverages: raspberry, cream and vanilla;

for hot cocoa-based beverages: raspberry, amaretto, cream, chocolate and vanilla;

for hot soups: mushroom, beef and chicken;

for cold beverages: coffee, tea, cherry, grape, and strawberry;

for dessert products: raspberry, chocolate, butterscotch, cherry, grape, strawberry, banana, and vanilla;

for other products: cheese, cream, seafood, meat, garlic and onion.

The aromatizing composition may also include one or more optional constituents such as a non-volatile edible fat or oil, a surfactant, a wetting agent, a foaming agent, an extremely volatile solvent, a propellant, dissolved edible solids, an antioxidant, or an aroma precursor. Although greater amounts may be used, the total amount of such additional constituents will not usually be more than about 100%, and preferably not more than about 40% by weight, based on the total weight of the carrier and aroma constituent. Suitable non-volatile edible fats or oils include coffee oil or other predominantly triglyceride oil used as a source of flavor or as a flavor solvent. A surfactant acts as a spreading agent or emulsifier to control the droplet size of the aromatizing composition and its degree of spreading on the surface of a food product. Suitable highly volatile solvents such as acetone and acetaldehyde act as a co-solvent for the volatile food aroma and modify the rate of evaporation of the aroma delivery system. A dissolved or entrapped propellant gas such as air, nitrogen, carbon dioxide, nitrous oxide, and the like, or a gas generator such as chemical carbonation reagents, may be included to increase buoyancy or to accelerate aroma release and evaporation. Dissolved edible solids increase the viscosity of the composition. Antioxidant additives such as BHA, BHT, TBHQ, vitamins A, C and E and derivatives, and various plant extracts such as those containing carotenoids, tocopherols or flavonoids having antioxidant properties, may be included to increase the shelf-life of the aromatized carrier. Aroma precursors that would not react during storage but would react to generate aroma during food preparation may also be included in the aromatizing composition.

The nature and amount of each optional ingredient that is included in the aromatizing composition is also dependent on the food product intended to be aromatized. For example, where a coffee oil or aromatized coffee oil is selected as an optional ingredient for an agent for aromatizing an instant coffee product, the amount of such coffee oil is preferably less than an amount that would give rise to an undesirable film of oil on the surface of the instant coffee beverage.

To facilitate floating of particles of the aromatizing composition on the surface of an aqueous beverage, density of the composition is suitably at least 0.6 and less than 1.0 g/cc and preferably from 0.7 to 0.99 g/cc and more preferably from 0.8 to 0.95 g/cc.

Although substantially limited by the physical properties of the carrier, the aromatizing compositions of the present invention may be formulated in a variety of ways. For example, natural or artificial flavoring agents, or mixtures thereof, may be used in combination with natural or synthetic carriers, or mixtures thereof, depending on the intended food product application and availability and cost of these ingredients. Some of the novel carriers disclosed can be obtained from natural, typically botanical sources, while others can only be obtained from synthetic, typically petroleum, sources. The same applies to the flavoring agents which are combined with the carriers.

In some applications, such as where the aromatizing composition will be used in an all-natural processed food product, flavoring agents and carriers must both be naturally sourced. In other, less restricted, applications, some or all of the components used to formulate the composition may be obtained from synthetic sources to alleviate limitations on availability or cost. Accordingly, the aromatizing compositions of the present invention may be produced, in forms described by U.S. labeling law, as a natural flavor or an artificial flavor. They may also be produced, in forms described by the convention commonly used in Europe, as a natural flavor or a nature identical flavor.

The aromatizing composition is physically entrapped in solid particles to protect the volatile carrier and volatile aroma from evaporation and deterioration. The aromatizing composition is preferably physically entrapped in solid particles by encapsulation, but may be simply absorbed such as by combining with an absorbent powdered food ingredient such as maltodextrin, or otherwise physically entrapped. Encapsulation is preferred because of the enhanced protection against evaporation and oxidation inherent in encapsulation. Encapsulation or other physical entrapment may be accomplished by any conventional technique, including those discussed in U.S. Pat. Nos. 5,339,368 and 5,750,178 mentioned above, the disclosure of each of which is herein incorporated by reference. A useful encapsulation technique is described in U.S. Pat. No. 4,520,033 and in Example 5 below. Other suitable encapsulation techniques are described in U.S. Pat. No. 5,496,574, and U.S. Pat. No. 3,989,852, the disclosure of each of which is incorporated by reference herein.

In general, any method of physical entrapment can be used that is effective in converting the aromatizing composition into particulate form. Preferred methods include co-extrusion, centrifugal co-extrusion, submerged nozzle co-extrusion, and the like which can be employed to produce a particulate containing a single continuous droplet of aromatizing composition, the size of which can be controlled to optimize evaporation characteristics. Less preferred methods include extrusion, spray drying, freeze-drying, absorption, adsorption, granulation, fluidized bed coating, inclusion complexation, and liposome entrapment. Any particulate produced by these methods that have undesirably small particle size or that contain finely emulsified and dispersed droplets may be advantageously agglomerated or granulated to increase the size and buoyancy of the particulate or to modify its dissolution rate in a food product.

The encapsulating material or the matrix material making up the solid particles into which the carrier is sorbed, may be any water soluble food grade material. Preferred water soluble encapsulation and matrix materials include soluble coffee solids, soluble tea solids, sugars, hydrolyzed starch products such as maltodextrins and corn syrup solids, hydrocolloids, and hydrolyzed proteins, as well as mixtures of these materials.

The particle size of the particulate aroma composition can vary widely. For most dehydrated food and beverage compositions, the particle size is suitably 0.1-10 mm, preferably 0.5-5 mm, and more preferably 1-3 mm.

For dehydrated beverage products, density of the particulate aroma composition is preferably sufficiently low to enable the particles to float in order to enhance the aroma release. However, in many instances a good aroma burst may be obtained for beverages when density of the aromatized particles is greater than that of water. For example, a good aroma burst can often be obtained with such particles when a hot liquid is poured into a particulate dehydrated beverage composition, or when the density of the particulate aromatizing composition or the density of the carrier, is sufficiently low to enable the particles or the carrier to rise very rapidly to the surface of the hot liquid. For dehydrated beverage products, absolute density of the aromatized particles, which determines if the particle will float in water, is preferably 0.2 to 0.99 g/cc, more preferably 0.3 to 0.95 g/cc, and still more preferably 0.4 to 0.9 g/cc, and bulk density which determines packing efficiency and is affected by particle size and shape, is preferably from 0.1 to 0.9 g/cc, more preferably from 0.2 to 0.8 g/cc, and still more preferably 0.3 to 0.7 g/cc. For non-beverage products, the absolute density of the aromatized particles may be higher than the density of water since the ability of the particles to float is not important. Similarly, their bulk density may be greater than 1.0 g/cc.

Bulk density of the particulate aroma composition is determined by pouring about 2-3 mL of the particles into a 10 mL graduated cylinder, vibrating until no further settling takes place, accurately noting both weight and volume and dividing the former by the latter to calculate bulk density to two decimal places. Absolute density is determined by adding very fine sand to the particles remaining in the cylinder after bulk density measurement and vibrating until all void spaces between the aromatized particles are filled with sand and no further settling takes place. The absolute density of the sand was first measured by filling a 10 mL cylinder with sand in the absence of aromatized particulates, vibrating until no further settling took place, accurately noting both weight and volume. The absolute density of the sand was calculated by dividing weight by volume to give a value of 1.66 g/cc. Knowledge of the absolute density of sand, individual weights of sand and particulates in the cylinder, and measurement of the volume and weight of the sand-particulate mixture allows calculation of the absolute density of the particles. Increased buoyancy can be obtained by gasifying the carrier, the solid matrix material, or both.

The amount of aromatizing composition present in the particulate aromatizing composition can vary considerably, but is generally maximized because it is generally the aroma constituent, and not the solid encapsulant or matrix that is desired to be incorporated into the food product. The aromatizing composition is preferably present in an amount of from about 1 to about 95% and more preferably from 10 to about 80% by weight based on the weight of the particulate aromatizing composition. However, where the solid material is also a component of the food product—such as where the solid particle is soluble coffee and the food product is a coffee beverage, the amount of solid material can be much larger. This can be very advantageous, e.g., in facilitating processing such as encapsulation. For such food products, the amount of solid material in the particulate aromatizing composition is suitably up to 95 or 99% by weight.

It is preferred, for simplicity, to utilize a single volatile carrier, but more than one may be employed in which case it is preferred that the selected carriers are miscible with one another. On the other hand, the aroma constituent is often made up of a plurality of aroma compounds as illustrated in several of the examples below.

The amount of the particulate aromatized composition suitable for incorporation into a dehydrated food product composition can vary widely, depending on several factors including the nature of the food composition, the nature and strength of the volatile food aroma, the nature and inherent aroma of the volatile carrier, and the nature and amount of the solid entrapping material and of any extraneous material. In general, the amount added is sufficient to provide good preparation aroma. In some cases, the dehydrated food product composition can be made up entirely of the particulate aromatized composition. For example, a furan carrier liquid, aromatized with a coffee frost, and encapsulated in soluble coffee capsules, can be formulated to constitute an instant coffee product. Accordingly, the particulate aromatized composition may constitute up to 100% by weight of the dehydrated food product composition. However, for most applications, it is suitable if the particulate aromatizing composition is present in an amount of from 0.05 to 50%, and for beverages typically 0.1-10% by weight, of the dehydrated food composition.

The dehydrated food product compositions in which the particulate aromatized composition of the present invention can be utilized can vary widely. Such compositions often include, in addition to one or more food ingredients, one or more optional agents such as bulking agents, fillers, sweeteners, creamers, flavoring agents, coloring agents, pH adjusting agents and buffers, gasifying agents, and the like. For particulate food compositions, the aromatized particles can be simply mixed with the food composition. In that event, it is preferred to match the density of the aromatized particles to that of the particulate dry-mix food composition in order to minimize segregation. For non-particulate food products, the aromatized particles can be included in the food product in any convenient way such as by physical incorporation, or as a separate ingredient which can be added by the consumer.

Foods are prepared from the dehydrated food product composition by rehydrating at a food preparation temperature. Hot beverages and soups are generally prepared at temperature of about 75-100° C. while cold beverages are generally prepared at temperatures ranging from 0 to 25° C. Iced beverages are often prepared by pouring a hot beverage solution over ice, in which case the initial burst of aroma is generated when the initial hot beverage solution is prepared. Desserts such as instant puddings and desserts are normally prepared with boiling or near boiling water.

EXAMPLE 1

This example demonstrates the ability to improve the appearance of an instant coffee beverage by replacement of coffee oil with a volatile flavor carrier according to this invention. Coffee oil has traditionally been used as an aroma carrier for instant coffee. However, like vegetable oils, this predominantly triglyceride oil is non-volatile and tends to float as small droplets that do not evaporate from the surface of a hot beverage. This does not normally pose a serious problem in instant coffee at the typically low use-levels needed to provide a package aroma. However, use of relatively high levels of aromatized coffee oil, typically needed to deliver a strong cup aroma, often produces an unsightly oil slick on the beverage. Replacement of aromatized coffee oil with aromatized d-limonene or other volatile carrier of this invention has been found to avoid this problem. These novel aromatized carriers similarly float as small droplets, but unlike coffee oil, they completely evaporate from the surface of the beverage without producing a residual oil slick.

Droplets of several liquids were provided on the surface of eight fluid ounces of water in a 400 mL beaker. Water temperature was maintained at 55, 65, 75, and 95° C. in four separate tests and effects were visually observed. Four different amounts (5, 10, 15 and 20 uL) of droplets of each liquid were applied at each test temperature. Droplets having a volume of about 5 uL to 10 uL (approximately 1-3 mm spheres) were produced by displacing four different amounts (5, 10, 15, and 20 uL) of each liquid from a 25 uL Hamilton Microliter fixed-needle syringe. Because a 10 uL displacement was needed to form a droplet that would fall from the syringe needle under its own weight, small volumes were delivered by touching the droplet that formed on the syringe needle to the surface of the water. Evaporation time for d-limonene was determined visually and was subject to variation since it is somewhat dependent on the method of addition, droplet size, presence of impurities, and the skill of the observer. Observed effects are reported in Table I and physical properties of the carriers are reported in Table II.

Table I summarizes the approximate visual rate of evaporation of the liquid droplets from the surface of hot water as a function of use-level and water temperature. It is evident that effective quantities of d-limonene will rapidly evaporate from hot beverages and other food products normally reconstituted with near-boiling water. Alternative volatile carriers of this invention having lower boiling point than d-limonene, such as 2-ethylfuran and ethyl acetate, beneficially evaporate much faster from the surface of hot water. In contrast, triacetin and benzyl alcohol, traditional flavor carriers, quickly sank to the bottom of the beverage in this test. Although volatile, these carriers have density greater than water and therefore can not be used in applications that require rapid surface evaporation. Ethanol and glycerol, two other widely used traditional flavor carriers, were also found to be unsuitable since they substantially dissolved in the water. By comparison, it can be seen from Table I that the low-density, substantially water-insoluble, volatile carriers of this invention are superior to traditional flavor carriers for producing the rapid surface evaporation needed to provide a desirable burst of aroma from hot beverages without producing a residual oil slick.

TABLE I Approximate rate of evaporation from 8 ounces hot water Evaporation Time (seconds) versus Water Temperature Carrier Volume 55° C. 65° C. 75° C. 95° C. d-limonene  5 μL 160  80 35 25 10 μL 180 115 55 40 15 μL 200 130 65 50 20 μL 225 135 70 55 coffee oil 5-20 μL Did not evaporate - produced unsightly oil slick. soybean oil 5-20 μL Did not evaporate - produced unsightly oil slick. 2-ethylfuran 5-20 μL Droplets rapidly evaporated from surface. ethyl acetate 5-20 μL Droplets rapidly evaporated from surface. triacetin 5-20 μL Droplets sank to bottom of beaker. benzyl alcohol 5-20 μL Droplets sank to bottom of beaker. ethanol 5-20 μL Droplets substantially dissolved in water. propylene glycol 5-20 μL Droplets substantially dissolved in water.

TABLE II Comparison of Physical Properties of Carriers Traditional Vapor Pressure* Boiling Point Density Water Suitable as Volatile Freezing Point Flavor Carriers (mm Hg) (° C.) (g/cc) Solubility Carrier (° C.) ethanol 59 78 0.79 miscible no −114 isopropanol ˜45 82 0.78 miscible no −89 propylene glycol 0.15 187 1.04 miscible no −60 triacetin <0.01 259 1.16 slight (7%) no 3 benzyl alcohol ˜0.05 205 1.04 slight (4%) no −15 acetoin ˜5 148 1.00 miscible no 15 soybean oil 0 none 0.92 insoluble no −10 triethyl citrate <0.01 294 1.14 insoluble no >10 glycerol <0.01 290 1.26 miscible no 18 water 24 100 1.0 miscible no 0 Novel Volatile Carriers d-limonene 2.1 175 0.84 insoluble yes −74 2-ethylfuran ˜50 92 0.91 insoluble yes <−70 ethyl acetate 94 77 0.90 slight (8%) yes −84 *Includes values reported in the literature and estimates based on available data. Vapor pressure, density, and water solubility (weight %) reported at 25° C..

EXAMPLE 2

This example demonstrates the ability to further improve the performance of d-limonene as a volatile carrier in a hot beverage application. This low-polarity monoterpene hydrocarbon has been found to possess the lowest odor impact among common terpenes. The product of commerce is sourced from citrus peel and contains a variety of more highly polar impurities including odiferous oxygenated terpenes and aliphatic compounds such as alcohols and aldehydes that give d-limonene a fruity odor. For non-fruity foods or beverages, for example instant coffee beverages, it is preferred to remove as much of these polar impurities as practically possible to minimize their potential impact on beverage flavor and aroma. It was found that filtering commercial d-limonene through a column packed with silica gel, activated carbon, Florisil™, or mixtures of these adsorbents was effective in virtually eliminating impurities, confirmed by gas chromatography analysis and trained panel organoleptic evaluations. Addition of 10-20 μL of unpurified (97-99.7% purity) d-limonene obtained from several sources, including Citrus & Allied Essences LTD, Sigma-Aldrich Co., and Firmenich Inc., onto the surface of hot water produced perceptible orange-lemon-lime odor, slight beverage flavor, and no residual surface oil. After purification, the color of these d-limonene products was generally transformed from pale-yellow to clear-white, their odor impact was greatly reduced upon evaporation from hot water, and their flavor impact in water was reduced to below the threshold of perception.

EXAMPLE 3

This example demonstrates the ability to improve the performance of a volatile carrier in a hot beverage application by choosing a carrier that has inherent odor particularly suited to the beverage. The very mild citrus aroma of purified d-limonene is particularly compatible with fruit-flavored beverages and the like, but somewhat less suitable for more subtly flavored beverages such as instant coffee. Furan and a variety of alkyl-substituted furans occur naturally in coffee and were found to have inherent odor better suited than d-limonene for use in instant coffee and related beverages. In particular, coffee flavors compounded into 2-methylfuran, 2-ethylfuran, 2,5-dimethylfuran, or mixtures were judged by trained panelists to produce aromas, when added to hot instant coffee beverages, that are better balanced than the same flavors compounded into d-limonene. These volatile carriers can be obtained from coffee only in very small quantities. Alternatively, they can be sourced from flavor houses and specialty chemical companies. The purification process described in Example 2 was found to significantly improve the quality and performance of these liquids, sourced from Aldrich Chemical Flavors & Fragrances, when employed as aroma carriers. Filtration through adsorbents generally transformed their pale-yellow color to clear-white and greatly reduced residual odor and flavor attributed to impurities and oxidation products present in the starting materials. No residual surface oil was observed in these tests.

EXAMPLE 4

This example demonstrates the ability to compound flavors into the volatile carriers of this invention for use in delivering an aroma. In order to demonstrate the utility of these novel carriers, a multi-component model flavor was compounded into a variety of carrier liquids to permit quantitative analysis of aroma release. A diverse mixture of six components was utilized in the model flavor in order to span a wide range of boiling point, water solubility, density, and chemical functionality. The model flavor was compounded into a number of traditional and novel carrier liquids having a wide range of properties. Two traditional carriers, soybean oil and ethanol, having very different physical properties were chosen along with three novel carriers of this invention, d-limonene, 2-ethylfuran, and ethyl acetate. Soybean oil was used as a reference carrier to depict the general performance of non-volatile triglyceride oils such as coffee oil. Each flavor component was present at a level of 5% wt/wt in the carrier, for a total flavor concentration of 30% wt/wt flavor in all carriers. Aroma release was quantified by injecting the aromatized carriers into an empty 50 mL dry jar preheated to 85° C. and, in another experiment, into a 250 mL jar containing 200 mL water preheated to 85° C. In each case, the internal headspace of the jar was rapidly swept with nitrogen gas and analyzed using a GC/MS (gas chromatography/mass spectroscopy) technique to measure the amount of each flavor that evaporated over time to produce aroma.

Tables III and IV detail the composition and physical-chemical properties of the model flavor components and carriers studied.

TABLE III Physical-Chemical Properties of Model Flavor Components Flavor Chemical Chemical Boiling Water Freezing Component Classification Formula Point (° C.) Density Solubility Point (° C.) 2-methylpropanal aldehyde C₄H₈O 64 0.79 low (10%) −66 diacetyl ketone C₄H₆O₂ 88 0.99 moderate −2 (20%) 2-ethylfuran heterocyclic C₆H₈O 92 0.91 insoluble isobutyl acetate ester C₆H₁₂O₂ 118 0.87 very low −99 (0.5%) 4-ethylguaiacol aromatic C₉H₁₂O₂ 235 1.06 very low 15 alcohol eugenol oxygenated C₁₀H₁₂O₂ 255 1.07 insoluble −9 monoterpene All flavor components are present in coffee aroma. Solubility data are approximate.

TABLE IV Physical-Chemical Properties of Carriers Chemical Chemical Boiling Water Freezing Carrier Classification Formula Point (° C.) Density Solubility Point (° C.) ethanol alcohol C₂H₆O 78 0.79 miscible −114 ethyl acetate ester C₄H₈O₂ 77 0.90 low (10%) −83 2-ethylfuran heterocyclic C₆H₈O 92 0.91 insoluble d-limonene monoterpene C₁₀H₁₆ 175 0.84 insoluble −74 hydrocarbon soybean oil triglyceride N/A N/A 0.92 insoluble −10 Soybean oil is Wesson brand soybean oil.

Table V summarizes the total recovery of flavor as aroma released from each carrier in both dry and wet systems.

TABLE V Total Model Aroma Recovery from Heated Jar Experiments Percent of Model Flavor Evaporated as Aroma during 2-Minutes after Addition to Jar ethyl Test Type soybean oil ethanol 2-ethylfuran d-limonene acetate Dry Jar 62% 72% 81% 78% 48% Wet Jar 40% 23% 41% 33% 29% All data are averages of two duplicate analyses. Total does not include response for 2-ethylfuran.

It can be seen that significantly less aroma was released from carriers, especially from water-miscible ethanol, in contact with hot water than from carriers injected into the hot dry jar. This may be attributable to fractional partitioning or dissolution of the flavor in water. Surface oil was observed with the soybean oil sample but not with the other samples.

Table VI compares the release rate of two aroma components that significantly contribute to perceived coffee freshness, 2-methylpropanal and diacetyl, from all carriers when injected into the heated dry jar.

TABLE VI Selected Model Component Aroma Release Rate from Hot Dry Jar Time Segment GC Headspace Counts (1x10E6) versus Flavor Carrier 2-methyl- soybean ethyl propanal oil ethanol 2-ethylfuran d-limonene acetate 0-10 sec 256 262 430 432 408 10-20 sec 297 418 405 368 403 20-30 sec 209 350 203 205 202 0-30 sec 762 1,030   1,038   1,005   1,012   30-60 sec 262 231 252 183 149 60-90 sec 111  54  31  35   24 90-120 sec  53  20  14  21   13 0-120 sec 1,188   1,335   1,335   1,244   1,198   soybean ethyl diacetyl oil ethanol 2-ethylfuran d-limonene acetate 0-10 sec 201 210 309 277 497 10-20 sec 223 256 315 259 498 20-30 sec 183 239 179 178 237 0-30 sec 607 705 803 714 1,232   30-60 sec 210 191 199 173 178 60-90 sec 129  69  42  60  38 90-120 sec  72  28  22  37  11 0-120 sec 1,018   993 1,066   984 1,459   All data are averages of two duplicate analyses.

It can be seen that, in general, the volatile carriers, d-limonene, 2-ethylfuran, and ethyl acetate produced a greater initial aroma burst than the soybean oil and ethanol references. Their peak evaporation rates occurred instantaneously for 2-methylpropanal, from 0-10 seconds, with strong continued release through the 10-20 second time segment. Conversely, peak evaporation rates of the reference carriers were somewhat delayed, occurring during the 10-20 second time segment. For diacetyl, the volatile carriers produced more rapid and sustained evaporation during the 0-20 second time segment, and d-limonene produced more rapid peak evaporation from 0-10 seconds. No residual surface oil was observed, except in the aromatized soybean oil samples.

EXAMPLE 5

This example discloses a method to aromatize and encapsulate volatile carriers into a particulate form that can be used to enhance aroma release from an instant coffee beverage upon reconstitution in hot water. Instant Maxwell House® Coffee was reconstituted in water to produce a 50% wt/wt solution. For each model coffee flavor system described in Example 4, 7.0 g of aromatized carrier was combined with 42.0 g of coffee solution and encapsulated using the following process. The coffee solution was cooled to 5° C. and aerated by mixing at 10,000 rpm for one minute using a Fisher Scientific PowerGen 700D immersion mixer. The aromatized carrier was then added and mixed at 10,000 rpm for one minute, sufficient to emulsify those aromatized carriers that are immiscible in water. The aromatized Coffee solution was added drop-wise from a syringe fitted with a 24-gauge needle into liquid nitrogen to form small frozen particles. These particles were separated from the liquid nitrogen and added to an excess quantity of finely milled instant coffee powder. Upon warming and slow desiccation in this powder over two days, the frozen particles were transformed into dry solid coffee capsules containing the aromatized carrier within a hard glassy shell. Aeration of the cold coffee solution prior to addition to liquid nitrogen was conducted to produce capsules having density less than 1.0 g/cc that float to maximize aroma release when added to hot water. Mixing and aeration can be conducted in an inert atmosphere to minimize oxidation of sensitive flavors.

Approximately 0.1 g quantities of 10-12 mesh size capsules were added to eight ounces of 85° C. water in a sealed jar and the headspace analyzed using the method described in Example 4. Sieve size here and elsewhere in this specification are U.S. standard sieve size, unless otherwise indicated. Particle size of the particles was 1.7-2 mm. All experiments were conducted in duplicate and the data averaged and normalized to exactly 0.1 g capsule weight.

Tables VII-IX summarize the aroma release rate of each model system component from the coffee capsules during the first three 10-second periods. Because the capsules do not dissolve instantaneously upon contact with hot water, it is to be expected that proportionately less evaporation occurs during the first 10-second period and that the greatest relative error in aroma analysis occurs during this time period.

TABLE VII Aroma Release from Capsules in Heated Water - 0-10 Seconds GC Headspace Counts (1x10E6) versus Flavor Carrier Flavor soybean ethyl Component oil ethanol 2-ethylfuran d-limonene acetate 2-methyl- 5.6 7.8 61.3 15.8 27.5 propanal diacetyl 3.0 1.3 18.5 5.1 20.2 2-ethylfuran 10.1 26.5 — 38.0 59.6 isobutyl acetate 7.9 33.7 119 27.9 63.3 4-ethylguaiacol 2.3 9.6 16.9 4.2 6.0 eugenol 2.4 8.4 24.4 3.8 4.0 Total 21.2 60.8 240.1 56.8 121.0 versus oil 1.00x 2.87x 11.33x 2.68x 5.72x All data are averages of two duplicate analyses. Total does not include response for 2-ethylfuran.

TABLE VIII Aroma Release from Capsules in Heated Water - 10-20 Seconds GC Headspace Counts (1x10E6) versus Flavor Carrier Flavor soybean ethyl Component oil ethanol 2-ethylfuran d-limonene acetate 2-methyl- 52.4 33.8 185 149 152 propanal diacetyl 18.5 6.2 81.0 46.6 89.8 2-ethylfuran 153 127 — 377 332 isobutyl acetate 114 163 464 377 411 4-ethylguaiacol 4.8 9.4 36.2 20.9 23.7 eugenol 3.2 8.3 18.7 18.4 18.0 Total 192.9 220.7 784.9 611.9 694.5 versus oil 1.00x 1.14x 4.07x 3.17x 3.60x All data are averages of two duplicate analyses. Total does not include response for 2-ethylfuran.

TABLE IX Aroma Release from Capsules in Heated Water - 20-30 Seconds GC Headspace Counts (1x10E6) versus Flavor Carrier Flavor soybean ethyl Component oil ethanol 2-ethylfuran d-limonene acetate 2-methyl- 126 76.8 158 247 131 propanal diacetyl 46.3 18.4 88.7 77.7 84.3 2-ethylfuran 358 231 — 582 319 isobutyl acetate 337 317 695 666 417 4-ethylguaiacol 56.6 21.7 64.0 38.1 23.3 eugenol 9.7 24.9 74.0 30.1 16.8 Total 575.6 458.8 1,079.7 1,058.9 672.4 versus oil 1.00x (0.80x) 1.88x 1.84x 1.17x All data are averages of two duplicate analyses. Total does not include response for 2-ethylfuran.

Tables X-XIII summarize the aroma release rate of each model system component from the coffee capsules during the four 30-second increments of the analysis.

TABLE X Aroma Release from Capsules in Heated Water - 0-30 Seconds GC Headspace Counts (1x10E6) versus Flavor Carrier Flavor soybean d- ethyl Component oil ethanol 2-ethylfuran limonene acetate 2-methylpropanal 184.0 118.4 404.3 411.8 310.5 diacetyl 67.8 25.9 188.2 129.4 194.3 2-ethylfuran 521.1 384.5 — 997.0 710.6 isobutyl acetate 458.9 513.7 1,278 1,070.9 891.3 4-ethylguaiacol 63.7 40.7 117.1 63.2 53.0 eugenol 15.3 41.6 117.1 52.3 38.8 Total 789.7 740.3 2,104.7 1,727.6 1,487.9 versus oil 1.00x (0.94x) 2.67x 2.19x 1.88x All data are averages of two duplicate analyses. Total does not include response for 2-ethylfuran.

TABLE XI Aroma Release from Capsules in Heated Water - 30-60 Seconds GC Headspace Counts (1x10E6) versus Flavor Carrier Flavor soybean d- ethyl Component oil ethanol 2-ethylfuran limonene acetate 2-methylpropanal 312 160 254 485 165 diacetyl 119 53.4 158 135 143 2-ethylfuran 853 441 — 1,017 502 isobutyl acetate 993 641 916 1,379 673 4-ethylguaiacol 91.6 71.2 145 1,030 66.4 eugenol 59.8 80.8 190 117 62.3 Total 1,575.4 1,006.4 1,663.0 2,219 1,109.7 versus oil — (0.64x) 1.06x 1.41x (0.70x) All data are averages of two duplicate analyses. Total does not include response for 2-ethylfuran.

TABLE XII Aroma Release from Capsules in Heated Water - 60-90 Seconds GC Headspace Counts (1x10E6) versus Flavor Carrier Flavor soybean d- ethyl Component oil ethanol 2-ethylfuran limonene acetate 2-methylpropanal 151 56.8 47.4 100 45.6 diacetyl 82.1 30.0 45.8 57.6 54.1 2-ethylfuran 539 199 — 331 276 isobutyl acetate 610 264 188 436 357 4-ethylguaiacol 88.9 58.5 109 113 77.7 eugenol 62.8 54.4 128 123 66.0 Total 994.8 463.7 518.2 829.6 600.4 versus oil — (0.47x) (0.52x) (0.83x) (0.60x) All data are averages of two duplicate analyses. Total does not include response for 2-ethylfuran.

TABLE XIII Aroma Release from Capsules in Heated Water - 90-120 Seconds GC Headspace Counts (1x10E6) versus Flavor Carrier Flavor soybean d- ethyl Component oil ethanol 2-ethylfuran limonene acetate 2-methylpropanal 105 23.6 19.2 41.7 23.5 diacetyl 78.1 20.3 28.8 35.6 34.7 2-ethylfuran 378 71.8 — 107 135 isobutyl acetate 382 97.2 75.2 162 145 4-ethylguaiacol 102 74.4 88.2 102 54.8 eugenol 73.9 57.1 104 77.0 40.4 Total 741.0 272.6 315.4 418.3 298.4 versus oil 1.00x (0.37x) (0.43x) (0.56x) (0.40x) All data are averages of two duplicate analyses. Total does not include response for 2-ethylfuran.

Table XIV summarizes aroma release for each component during the full two-minute analysis while Table XV summarizes cumulative release during each time segment analyzed.

TABLE XIV Cumulative Aroma Release from Capsules in Heated Water - 0-120 Seconds Cumulative GC Headspace Counts (1x10E6) versus Flavor Carrier Flavor soybean d- ethyl Component oil ethanol 2-ethylfuran limonene acetate 2-methylpropanal 752.0 358.8 724.9 1,038.5 544.6 diacetyl 347.0 129.6 420.8 357.6 426.1 2-ethylfuran 2,291.1 1,096.3 — 2,452.0 1,623.6 isobutyl acetate 2,443.9 1,515.9 2,457.2 3,047.9 2,066.3 4-ethylguaiacol 346.2 244.8 459.3 381.2 251.9 eugenol 211.8 233.9 539.1 369.3 207.5 Total 4,100.9 2,483.0 4,601.3 5,194.5 3,496.4 versus oil 1.00x (0.61x) 1.12x 1.27X (0.85x) All data are averages of two duplicate analyses. Total does not include response for 2-ethylfuran.

TABLE XV Total Aroma Release from Capsules in Heated Water versus Time Total GC Headspace Counts (1x10E6) versus Flavor Carrier Time soybean ethyl Segment oil ethanol 2-ethylfuran d-limonene acetate  0-10 sec 21.2 60.8 240.1 56.8 121.0 10-20 sec 192.9 220.7 784.9 611.9 742.7 20-30 sec 575.6 458.8 1,079.7 1,058.9 721.3  0-30 sec 789.7 740.3 2,104.7 1,727.6 1,585.0 30-60 sec 1,575.4 1,006.4 1,663.0 2,219.0 1,187.4 60-90 sec 994.8 463.7 518.2 829.6 642.7 90-120 sec  741.0 272.6 315.4 418.3 320.4 0-120 sec 4,100.9 2,483.0 4,601.3 5,194.5 3,735.5 versus oil 1.00x (0.61x) 1.12x 1.27x (0.91x) All data are averages of two duplicate analyses. Total does not include response for 2-ethylfuran.

Table XVI summarizes aroma release normalized against the release from the soybean oil reference.

TABLE XVI Normalized Aroma Release from Capsules in Heated Water versus Time Normalized Total GC Headspace Counts (1x10E6) versus Flavor Carrier Time soybean ethyl Segment oil ethanol 2-ethylfuran d-limonene acetate  0-10 sec 1.00x 2.87x 11.33x 2.68x 5.72x 10-20 sec 1.00x 1.14x 4.07x 3.17x 3.60x 20-30 sec 1.00x (0.80x) 1.88x 1.84x 1.17x  0-30 sec 1.00x (0.94x) 2.67x 2.19x 1.88x 30-60 sec 1.00x (0.64x) 1.06x 1.41x (0.70x) 60-90 sec 1.00x (0.47x) (0.52x) (0.83x) (0.60x) 90-120 sec  1.00x (0.37x) (0.43x) (0.56x) (0.40x) 0-120 sec 1.00x (0.61x) 1.12x 1.27x (0.85x) All data are averages of two duplicate analyses. Total does not include response for 2-ethylfuran.

TABLE XVII Physical Properties of Particles Aromatizing Composition Particulate % % Density Size Bulk Density Absolute Density Flavor Carrier Flavor Carrier (g/cc) (mm) (g/cc) (g/cc) model coffee soybean oil 30 70 0.93 1.7-2.0 0.54 0.62 model coffee ethanol 30 70 0.84 1.7-2.0 0.58 0.89 model coffee 2-ethylfuran 30 70 0.92 1.7-2.0 0.53 0.67 model coffee d-limonene 30 70 0.87 1.7-2.0 0.48 0.66 model coffee ethyl acetate 30 70 0.91 1.7-2.0 0.54 0.68

It can be seen that the preferred water-insoluble volatile carriers of this invention performed significantly better than the soybean oil reference on all measures. Ethanol performed relatively poorly, attributable to miscibility of this carrier with water. Ethyl acetate performance was intermediate, with strong initial aroma release being somewhat compromised by less total aroma release due to the slight solubility of this carrier in water. Most importantly, the volatile carriers of this invention released significantly more aroma in the critical first 30 seconds than the soybean oil reference without producing residual surface oil.

EXAMPLE 6

This example demonstrates enhanced release of a complex artificial coffee aroma when compounded into a novel volatile carrier and encapsulated according to the method of Example 5. An artificial coffee flavor containing over 20 components was compounded by an experienced flavorist into several different carrier liquids. The concentration of flavor in each carrier was constant at approximately 30% wt/wt. A mixture of two traditional carriers, propylene glycol and ethanol, was compared to two different novel volatile carriers of this invention, d-limonene and 2-ethylfuran. Each system was encapsulated in the coffee matrix according to the method described in Example 5. The capsules were similarly sized and equal amounts added to hot water. An experienced panel concluded that capsules containing flavor compounded into 2-ethylfuran produced the strongest aroma burst, followed by capsules containing flavor compounded into d-limonene. No surface oil was observed with either of these capsules. Capsules containing flavor compounded into the mixture of propylene glycol and ethanol did not provide a strong aroma burst.

EXAMPLE 7

This example demonstrates the utility and versatility of this invention in producing encapsulated flavors with enhanced aroma release properties for use in specialty beverages. Several different complex flavors were individually compounded by experienced flavorists into d-limonene and 2-ethylfuran and encapsulated in a coffee matrix according to the method described in Example 5. Freeze-dried Kenco™ Really Rich coffee was reconstituted with water to make a 50% wt/wt coffee solution and the capsules were dried in a finely milled powder of the same coffee. Capsules containing hazelnut, chocolate, raspberry, amaretto, vanilla, and cream flavors were produced. The capsules were sized into several different ranges: 4-6 mesh; 6-8 mesh; 8-10 mesh; and 10-14 mesh. Performance was evaluated by combining 0.15 g capsules with 20 g Maxwell House Cafe® Cappuccino® powder and reconstituting in 8 oz. near-boiling water. The capsules dissolved and delivered a strong aroma burst. The smaller capsules dissolved more rapidly than larger capsules to provide faster aroma release. An experienced panel concluded that, in general, the capsules containing flavors compounded into 2-ethylfuran produced a stronger aroma burst than capsules containing flavors compounded into d-limonene. Dissolution of the floating coffee capsules produced a desirable marbleized foam core. No residual surface oil was observed in these tests.

EXAMPLE 18

This example demonstrates the ability to encapsulate flavors in a white capsule matrix that does not produce brown color spots or streaks in a cappuccino foam. A mixture of 25.2 g 24DE corn syrup solids and 2.0 g VersaWhip 600K hydrolyzed soy protein (Quest International) was dissolved in 14.8 g water. The cream flavor described in Example 7 was individually compounded into d-limonene and 2-ethylfuran. Seven grams of the aromatized carriers were emulsified into the 42.0 g solutions, then dropped into liquid nitrogen to form frozen particles. The particles were then separated from the liquid nitrogen and dried in an excess amount of powdered 1 ODE corn maltodextrin for 48 hours. Bulk density of the particles was about 0.3 g/cc. When sized and evaluated in Maxwell House Cafe® Cappuccino® according to the method of Example 7, the capsules dissolved and delivered a strong aroma burst without discoloring the predominantly white foam and without leaving surface oil. An experienced panel concluded that, in general, the capsules containing flavors compounded into 2-ethylfuran produced a stronger aroma burst than capsules containing flavors compounded into d-limonene. Similar capsules made without hydrolyzed soy protein had a bulk density of about 0.55 g/cc, were not sufficiently soluble, and did not rupture quickly when added to hot water. It was found that hydrolyzed milk protein or gelatin could similarly be used in place of the hydrolyzed soy protein to allow greater incorporation of gas in the solution during mixing, resulting in lower capsule density and an increased rate of dissolution. It was also found that optional use of surface-active agents such as polysorbate 60/80 could be used to further speed capsule dissolution.

EXAMPLE 9

This example demonstrates the ability to enhance the aroma of a hot instant tea beverage. The process of Example 7 was used to prepare coffee capsules containing an amaretto flavor compounded into d-limonene. The capsules were sized to 6-8 mesh and 0.15 g added to 2.0 g Lipton 100% Instant Tea power. Reconstitution in 8 oz. of near-boiling water produced a strong burst of amaretto aroma. The use of these floating coffee capsules did not adversely affect beverage appearance or flavor, and there was no residual surface oil. The same amaretto flavor was compounded into d-limonene and encapsulated in instant tea by substituting tea for coffee according to the process of Example 5. Similar evaluation of the 6-8 mesh tea capsules produced a strong burst of amaretto aroma without adversely affecting beverage appearance or flavor, and there was no residual surface oil.

EXAMPLE 10

This example demonstrates the ability to enhance the aroma of a hot soup mix. The process of Example 8 was used to prepare white capsules containing a cream flavor compounded into 2-ethylfuran. The capsules were sized to 6-8 mesh and 0.15 g added to 11.0 g Lipton Spring Vegetable Cup-a-Soup® instant soup mix. Reconstitution in 6 oz. of boiling water produced a strong burst of cream aroma. The use of floating white capsules did not adversely affect soup appearance or flavor and no significant residual cream flavor was detected. No residual surface oil was observed.

EXAMPLE 11

This example demonstrates the ability to enhance the aroma of a hot cocoa mix. An amaretto flavor was compounded into d-limonene and encapsulated in instant coffee according to the process of Example 5. The capsules were sized to 6-8 mesh, and 0.15 g of the capsules were added to 12.0 g Swiss Miss® Hot Cocoa mix (Hunt-Wesson Inc.) Reconstitution in eight ounces of boiling water produced a strong burst of amaretto aroma without adversely affecting beverage appearance or flavor. No residual surface oil was observed.

EXAMPLE 12

This example demonstrates the ability to use a variety of other volatile carriers of this invention to enhance the aroma of a hot cider beverage. Several almond-cherry flavor systems were prepared by compounding 1 part benzaldehyde into 3 parts of volatile carrier. Benzaldehyde was compounded into 3-heptanone, methyl hexanoate, 1-octanol, and octanal and the process of Example 8 was used to prepare white capsules containing the almond-cherry flavor in each of these four volatile carriers. Physical properties of the volatile carriers are reported in Table XVIII. The capsules were sized to 6-8 mesh and 0.15 g added to 8 oz. portions of Dominick's (Safeway) brand pasteurized Apple Cider that had been pre-heated to 85° C. The floating capsules produced a burst of almond-cherry aroma. The greatest aroma intensity and best aroma/carrier balance was obtained from 3-heptanone and methyl hexanoate. No residual surface oil was observed.

TABLE XVIII Physical Properties of Carriers Novel Vapor Boiling Freezing Volatile Pressure* Point Water Chemical Point Carriers (mm Hg) (° C.) Density (g/cc) Solubility Classification (° C.) octanal ˜2.4 173 0.83 insoluble aldehyde −12 1-octanol ˜0.05 195 0.83 insoluble aliphatic alcohol −16 3-heptanone ˜3.7 149 0.82 insoluble ketone −39 methyl ˜4.0 151 0.89 insoluble ester −71 hexanoate *Includes values reported in the literature and estimated based on available data. Vapor pressure, density, and water solubility (weight %) reported at 25° C.

EXAMPLE 13

This example demonstrates the ability to enhance the preparation aroma of gelatin dessert mixes. A mixture of 25.2 g 24DE corn syrup solids, 2.0 g VersaWhip 600K, and 0.2 g polysorbate 80 was dissolved in 14.6 g water to prepare a solution. A raspberry flavor was compounded into ethyl acetate and 7.0 g of the aromatized carrier emulsified into 42.0 g of the solution, then dropped into liquid nitrogen to form frozen particles. The particles were then separated from liquid nitrogen and dried in an excess amount of powdered 10DE corn maltodextrin for 48 hours. The white capsules were sized to 8-10 mesh and 0.2 g dry-mixed with 8.5 g Jell-O® brand Sugar Free Raspberry artificially flavored gelatin dessert mix in a bowl. Upon addition of ¾ cup boiling water to the mixture, the capsules floated and dissolved to deliver a strong raspberry aroma. Similar reconstitution of the mix without addition of flavor capsules produced a weaker raspberry aroma. The same capsules were evaluated in Jell-O® brand Sparkling White Grape artificially flavored gelatin dessert. Addition of 0.2 g of the capsules to 83 g gelatin mix and similar reconstitution in boiling water produced a strong raspberry aroma. No residual surface oil was observed in these tests.

EXAMPLE 14

This example demonstrates the ability to enhance the aroma of an instant oatmeal product. A 0.2 g portion of the raspberry capsules described in Example 13 was dry-mixed with 28 g of Quaker™ Instant Oatmeal in a bowl. Upon addition of ⅔ cup boiling water to the mixture, the capsules dissolved and released a strong raspberry aroma. No residual surface oil was observed. Similar rehydration of the oatmeal without addition of flavor capsules produced a weak cereal aroma.

EXAMPLE 15

This example demonstrates the ability to enhance the aroma of a flavored coffee beverage. A 0.2 g mixture of equal amounts of two different 6-8 mesh capsules was mixed with 16 g General Foods® International Coffees—Swiss White Chocolate artificial flavor Swiss style flavored instant coffee. Raspberry flavor compounded into ethyl acetate and chocolate flavor compounded into d-limonene were individually encapsulated according to the method of Example 8. Upon addition of 8 oz. near-boiling water to the mixture, the capsules floated and dissolved to deliver a strong raspberry chocolate aroma. Similar reconstitution of the mix without addition of flavor capsules produced a mild milk chocolate type aroma. No residual surface oil was observed in these tests.

EXAMPLE 16

This example demonstrates the advantage of using volatile carriers of this invention to prepare a genuine coffee aroma when a coffee frost is used as the aroma source. Coffee oil is typically aromatized by direct contact with a condensed frost while heating to prevent the oil from freezing. Unfortunately, heating causes a substantial evaporative loss of aroma, particularly of desirable highly volatile and labile components that contribute disproportionately to coffee freshness and quality. It was found that because the novel volatile carriers of this invention typically have freezing points much lower than triglyceride oils, they can be aromatized by direct contact with coffee frosts without the need for heating. This was successfully demonstrated for two novel carriers, d-limonene and 2-ethylfuran. The carriers were first purified using the method described in Example 2 and then utilized to prepare four different aromatized carriers using the following procedure.

Two different characteristically yellow frosts were obtained from grinding or steaming roasted coffee and condensing the volatiles at a temperature below the freezing point of carbon dioxide, the principal component of coffee frosts. Each of the purified colorless carriers was chilled to about 5° C. and individually directly contacted with the two different frosts for a period of time sufficient for the frosts to melt and for the coffee aroma components to reach equilibrium with the carriers. The carriers did not freeze upon contact with the frosts and possessed adequate solvation capacity to become highly aromatized with coffee components, evidenced by their acquired yellow colors. In fact, this method produced completely volatile, genuine aroma systems having significantly higher coffee aroma concentration and odor impact than coffee oil aromatized using traditional means. Their high aroma contents were confirmed using GC analysis and organoleptic evaluation. The aromatized carriers were encapsulated in a coffee matrix according to the procedure described in Example 5. When sized and mixed with instant coffee and reconstituted in hot water, the capsules produced a strong burst of high-quality, fresh coffee aroma that could not be achieved by similar encapsulation of an equal amount of conventionally aromatized coffee oil. No residual surface oil was observed.

EXAMPLE 17

Droplets of a hazelnut flavor compounded into furan by an experienced flavorist are deposited, in the manner of Example 1, on the surface of a cold beverage prepared by reconstituting an unflavored General Foods International Coffees® Cappuccino Coolers® powder in cold skim milk. Furan has a vapor pressure of 600 mm Hg at 25° C., a boiling point of 31° C., a density of 0.95 g/cc at 25° C., a freezing point of −86° C., and is water insoluble. The aromatized carrier liquid evaporated from the surface of the beverage and produced a burst of above-cup aroma, with no residual surface oil. A good above-cup aroma burst will also be obtained by encapsulating or otherwise physically entrapping the aromatized carrier in a suitable cold water soluble solid particulate.

EXAMPLE 18

This example demonstrates the utility of this invention in producing encapsulated flavors with enhanced aroma release properties for use in roast and ground coffee preparation applications. One gram of the coffee capsules described in Example 16 containing 2-ethylfuran aromatized with roasted coffee bean grinder gas frost was mixed with 50 g Blå mocca Mellanrost Brygg™ roast and ground coffee. The mixture was placed in the filter basket of a Morphy Richards™ 12-cup coffee maker and brewed with one liter of water. The capsules dissolved in the filter basket upon contact with the percolating hot water and delivered an intense fresh coffee aroma burst of very good quality. An experienced panel judged the intensity and quality of this preparation aroma superior to the preparation aroma obtained from a similar 50 g/L preparation of the same coffee without capsule addition.

Dissolution and Flotation Time

The dissolution time, and the time taken to rise in water, of several of the particles described in the examples was determined by placing six particles in a sealed container secured at the bottom of a 250 mL beaker, and after adding 200 mL of near boiling water (90-95° C.) to the beaker, opening the top of the sealed container. The time taken for at least four of the six particles to reach the surface and the time taken for complete dissolution of the particles were measured by stopwatch. The sealed container was fabricated from the barrel of a syringe which was reduced in length to about ½ inch. The syringe plunger was employed to seal and to open the container. After adding the hot water to the beaker, the plunger was removed to open the sealed container and the stopwatch was started. The time at which the particles reached the surface and the time at which complete dissolution were reached was determined visually and measured by stopwatch. Results were as follows:

Particulate Time to Aromatizing Composition Bulk Absolute Time to Dissolve % % Density Size Density Density Float Completely Flavor Carrier Flavor Carrier (g/cc) mm (g/cc) (g/cc) (sec) (sec) coffee d-limonene 2.00 98.00 0.91 1.2-1.5 0.33 0.41 1 3 chocolate d-limonene 0.65 99.35 0.84 2.0-2.4 0.43 0.57 1 2 amaretto d-limonene 23.00 61.00 0.90 1.7-2.0 0.63 0.78 20 90 dairy cream 2-ethylfuran 38.50 61.50 0.99 1.7-2.0 0.64 0.79 5 45 cherry/ octanal 25.00 75.00 0.88 1.7-2.0 0.58 0.82 20 30 almond cherry/ 1-octanal 25.00 75.00 0.88 1.7-2.0 0.57 0.65 20 90 almond cherry/ methyl 25.00 75.00 0.93 1.7-2.0 0.56 0.80 20 90 almond hexanoate raspberry ethyl acetate 13.95 86.05 0.92 1.7-2.0 0.49 0.85 1 2 

What is claimed is:
 1. A particulate food preparation aroma composition comprising particles having a solid, water soluble matrix, said matrix having physically entrapped therein a food aromatizing composition, said food aromatizing composition comprising a volatile characterizing food aroma constituent other than a natural essential oil, and a volatile organic carrier, said volatile organic carrier being in the liquid state at 25° C. and atmospheric pressure, having a vapor pressure of at least 0.01 mm Hg at 25° C., a boiling point in the range of 25 to 250° C., a density less than 1.0 g/cc at 25° C., and water solubility of not more than about 10% at 25° C., said carrier is present in an amount of at least 25% by weight based on the total weight of the carrier and the aroma constitute.
 2. A particulate composition according to claim 1 wherein said carrier is present in an amount of at least 35% by weight based on the total weight of the carrier and the aroma constituent.
 3. A particulate composition according to claim 1 wherein said carrier is present in an amount of at least 50% by weight based on the weight of the carrier and the aroma constituent.
 4. A particulate composition according to claim 1 wherein said particles have an absolute density of 0.2 to 0.99 g/cc.
 5. A particulate composition according to claim 1 wherein the size of said particles is from 0.1 to 10 mm.
 6. A particulate composition according to claim 1 wherein said volatile carrier has a vapor pressure of at least 0.5 mm Hg at 25° C., a boiling point in the range of 25 to 200° C., a density of less than 1.0 g/cc at 25° C., and water solubility of not more than about 5% at 25° C.
 7. A particulate composition according to claim 1 wherein said volatile carrier has a vapor pressure of at least 2 mm Hg at 25° C., a boiling point in the range of 25-100° C., and a density in the range of 0.7-0.99 g/cc at 25° C., and wherein said volatile carrier is water insoluble.
 8. A particulate composition according to claim 7 wherein said volatile carrier has a density in the range of 0.8-0.95 g/cc at 25° C.
 9. A particulate composition according to claim 1 wherein said volatile carrier has a boiling point in the range of 25-50° C.
 10. A particulate composition according to claim 1 wherein said food aroma constituent is synthetic.
 11. A particulate composition according to claim 1 wherein said carrier is synthetic.
 12. A particulate composition according to claim 1 wherein said food aroma constituent and said carrier are synthetic.
 13. A particulate composition according to claim 1 wherein said particles comprise capsules having a solid water soluble capsule shell encapsulating said food aromatizing composition.
 14. A particulate composition according to claim 1 wherein said solid water soluble matrix is coffee-derived.
 15. A particulate composition according to claim 1 wherein said volatile carrier is selected from the group consisting of monoterpene hydrocarbons, esters, and alkyl furans.
 16. A particulate composition according to claim 1, wherein said volatile carrier is selected from the group consisting of d-limonene, 2-ethylfuran, 2-methylfuran, 2,5-dimethylfuran and ethyl acetate.
 17. A particulate composition according to claim 1 wherein said carrier comprises a plurality of compounds belonging to a common chemical classification group.
 18. A particulate composition according to claim 1 wherein said particles have an absolute density of 0.3 to 0.99 g/cc.
 19. A particulate composition according to claim 13 wherein said capsule shell comprises a material selected from the group consisting of sugars, hydrolyzed starch products, hydrocolloids, hydrolyzed proteins, soluble coffee and soluble tea.
 20. A particulate composition according to claim 1 wherein said aromatizing composition further comprises at least one optional ingredient selected from the group consisting of surfactants, dispersants, non-volatile edible fat or oils, volatile co-solvents, gaseous propellants, and dissolved edible solids, the total amount of said optional ingredients not exceeding 100% by weight based on the total weight of said carrier and said aroma constituent.
 21. A dehydrated food or beverage product comprising a food ingredient and a particulate food preparation aroma ingredient for providing a burst of aroma at the time of preparing a food or beverage from said dehydrated food or beverage product composition, said particulate food preparation aroma ingredient comprising particles having a solid, water soluble matrix, said matrix having physically entrapped therein a food aromatizing composition, said food aromatizing composition comprising a volatile characterizing food aroma constituent other than a natural essential oil, and a volatile organic carrier, said volatile organic carrier being in the liquid state at 25° C. and atmospheric pressure, having a vapor pressure of at least 0.01 mm HG at 25° C., a boiling point in the range of 25 to 250° C., a density less than 1.0 g/cc at 25° C., water solubility of not more than about 10% at 25° C., and present in an amount of at least 25% by weight based on the total weight of the carrier and the aroma constituent.
 22. A food or beverage product composition according to claim 21 wherein said food ingredient is particulate and wherein said composition is a dry-mix food product composition.
 23. A food or beverage product composition according to claim 22 wherein said particulate food ingredient comprises a member selected from the group consisting of soluble coffee and soluble tea.
 24. A food or beverage product composition according to claim 21 wherein said particulate food preparation aroma ingredient has a particle size of 0.1-10 mm.
 25. A food or beverage product composition according to claim 21 further comprising at least one member selected from the group consisting of sweeteners, creamers, bulking agents, fillers, flavoring agents, coloring agents, pH adjusting agents, buffers and gasifying agents. 